摘要
用流动法测定了四氢呋喃、水、１，４－丁二醇三元大沸点差体系汽液平衡，将实测数据与作者先前回归得到的二元体系Ｗｉｌｓｏｎ模型参数的推算值进行了比较，结果比较吻合。
The VaporLiquid equilibrium (VLE) data for the ternary system tetrahydrofuran(THF)water1,4butanediol (BD)were measured by the bubbleequilibrium still method at 50℃, 70℃, and 90℃, respectively. Estimation of the VLE data for the fernary system was made by three pairs of binarysystem Wilson parameters obtained from the authors former work. The calculation values were in good agneement with the experimental data.
出处
《天然气化工—C1化学与化工》
CAS
CSCD
北大核心
1998年第2期55-59,共5页
Natural Gas Chemical Industry
关键词
汽液平衡
四氢呋喃
水
丁二醇
三元系
Vaporliquid equilibrium, terahydrofuran(THF), water, butanediol(BD)
